US2503963A - Method for preparing a fischertropsch catalyst - Google Patents

Method for preparing a fischertropsch catalyst Download PDF

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Publication number
US2503963A
US2503963A US110472A US11047249A US2503963A US 2503963 A US2503963 A US 2503963A US 110472 A US110472 A US 110472A US 11047249 A US11047249 A US 11047249A US 2503963 A US2503963 A US 2503963A
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Prior art keywords
catalyst
approximately
mixture
preparing
hours
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Expired - Lifetime
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US110472A
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English (en)
Inventor
Max A Mosesman
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Standard Oil Development Co
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Standard Oil Development Co
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Filing date
Publication date
Priority to FR957261D priority Critical patent/FR957261A/fr
US case filed in Texas Western District Court litigation Critical https://portal.unifiedpatents.com/litigation/Texas%20Western%20District%20Court/case/6%3A20-cv-00670 Source: District Court Jurisdiction: Texas Western District Court "Unified Patents Litigation Data" by Unified Patents is licensed under a Creative Commons Attribution 4.0 International License.
Priority to US717587A priority patent/US2537688A/en
Priority claimed from US717583A external-priority patent/US2503964A/en
Priority claimed from US717586A external-priority patent/US2438449A/en
Priority to GB24246/47A priority patent/GB641261A/en
Application filed by Standard Oil Development Co filed Critical Standard Oil Development Co
Priority to US110472A priority patent/US2503963A/en
Application granted granted Critical
Publication of US2503963A publication Critical patent/US2503963A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/78Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali- or alkaline earth metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/843Arsenic, antimony or bismuth
    • B01J23/8435Antimony
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0425Catalysts; their physical properties
    • C07C1/043Catalysts; their physical properties characterised by the composition
    • C07C1/0435Catalysts; their physical properties characterised by the composition containing a metal of group 8 or a compound thereof
    • C07C1/044Catalysts; their physical properties characterised by the composition containing a metal of group 8 or a compound thereof containing iron
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/1512Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by reaction conditions
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/153Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used
    • C07C29/156Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used containing iron group metals, platinum group metals or compounds thereof
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/02Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the alkali- or alkaline earth metals or beryllium
    • C07C2523/04Alkali metals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/18Arsenic, antimony or bismuth
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74Iron group metals
    • C07C2523/745Iron
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
    • C07C2523/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/843Arsenic, antimony or bismuth
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Definitions

  • Patented Apr. 11, 1950 FICE METHOD FOR PREPARING A FISCHER- TROPSCH CATALYST Max A. Mosesman, Baytown, Ten, assignor, by l mesne assignments, to Standard Oil Development Company, Elizabeth, N. J., a corporation of Delaware No Drawing. Original application December 20,
  • This invention is directed to a method for preparing a composition adapted to be used as a catalyst. More particularly, this invention relates to a method for preparing a promoted cata-' lyst forutilization in the hydrogenation of carbon oxides.
  • Catalysts containing promoters in substantially small quantities often permit consistently high conversion of the reactants to desired products over much longer periods of operation than is possible when using an unpromoted catalyst.
  • a pertinent object of the present invention is to devise a method for preparing a catalyst particularly adapted for use in the Fischer-Tropsch synthesis.
  • Another object of this invention is to prepare a catalyst that may be utilized in the synthesis of high yields of useful products by the hydrogenation of carbon oxides during long periods of operation.
  • the present invention may be described briefly as involving the preparation of a catalyst comprising a major portion of iron or an iron oxide as the active catalyst material and a minor portion of alkali metal ferrate as the promoting material.
  • alkali metal ferrates include potassium ferrate (K2FeO4) sodium ferrate and lithium ferrate.
  • the present invention will be further illustrated by a method of preparing an iron oxide catalyst comprising an alkali metal ferrate promoter.
  • a previously dried intimate mixture of one part by weight of fine iron powder and two parts by weight of potassium nitrate was placed on an iron plate anddistributed as a layer of approximately 2 centimeters depth.
  • a second layer of approximately equal parts by weight of iron powder and potassium nitrate was then placed adjacent to the first layer. The second layer was then ignited and the reaction allowed to go to completion.
  • a dense white cloud of volatile potassium formed which was removed from the reaction zone.
  • the reaction product was cooled sufliciently for handling and removed from the iron plate and heated in a free oxygen containing atmosphere at approximately 1000 F. for about 4 hours.
  • the reaction product was ground into a fine powder and pilled into one-eighth inch pills. Subsequent to the pilling operation, the pills were placed in a reaction chamber and reduced in the presence of hydrogen for 24 hours at a temperature of 700 F. and at atmospheric pressure. The hydrogen was passed over the catalyst at a feed rate of hydrogen of 1000 volumes per volume of catalyst per hour.
  • The-catalyst prepared as described in the foregoing paragraph was then employed to synthesize hydrocarbons from an equal mixture of hydroen and carbon monoxide.
  • the feed mixture of hydrogen and carbon monoxide was passed over the catalyst at a premure of p. s. i. g., a temperature of 575 F. and at a feed rate of 200 volumes per volume of catalyst.
  • the catalyst prepared in accordance with this method of the present invention gives good yields of hydrocarbon and oxygenated compounds which may be obtained over substantial periods of operating time.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
US110472A 1946-12-20 1949-08-15 Method for preparing a fischertropsch catalyst Expired - Lifetime US2503963A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
FR957261D FR957261A (enrdf_load_html_response) 1946-12-20
US717587A US2537688A (en) 1946-12-20 1946-12-20 Method for synthesizing hydrocarbons and oxygenated compounds
GB24246/47A GB641261A (en) 1946-12-20 1947-09-02 An improved catalyst and method of producing same
US110472A US2503963A (en) 1946-12-20 1949-08-15 Method for preparing a fischertropsch catalyst

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US717583A US2503964A (en) 1946-12-20 1946-12-20 Preparation of an iron-alkali metal ferrate catalyst
US717586A US2438449A (en) 1946-12-20 1946-12-20 Synthesis of hydrocarbons and oxygenated compounds
US110472A US2503963A (en) 1946-12-20 1949-08-15 Method for preparing a fischertropsch catalyst

Publications (1)

Publication Number Publication Date
US2503963A true US2503963A (en) 1950-04-11

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US110472A Expired - Lifetime US2503963A (en) 1946-12-20 1949-08-15 Method for preparing a fischertropsch catalyst

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US (1) US2503963A (enrdf_load_html_response)
FR (1) FR957261A (enrdf_load_html_response)
GB (1) GB641261A (enrdf_load_html_response)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2684283A (en) * 1950-09-21 1954-07-20 Jr Richard A Ogg Method of recovering dilute nitrogen oxides from gaseous mixtures
CN114570412A (zh) * 2022-02-18 2022-06-03 贵州理工学院 一种费托芳烃催化剂和制备方法及用途

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4246910A (en) * 1977-08-01 1981-01-27 Philip Morris Incorporated Cigarette filter material comprising compounds of iron in high oxidation states

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB191402308A (en) * 1914-01-28 1915-07-29 James Yate Johnson Improvements in the Hydrogenisation and Dehydrogenisation of Compounds containing Carbon.
US2093504A (en) * 1934-09-20 1937-09-21 Ig Farbenindustrie Ag Manufacture of sulphides

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB191402308A (en) * 1914-01-28 1915-07-29 James Yate Johnson Improvements in the Hydrogenisation and Dehydrogenisation of Compounds containing Carbon.
US2093504A (en) * 1934-09-20 1937-09-21 Ig Farbenindustrie Ag Manufacture of sulphides

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2684283A (en) * 1950-09-21 1954-07-20 Jr Richard A Ogg Method of recovering dilute nitrogen oxides from gaseous mixtures
CN114570412A (zh) * 2022-02-18 2022-06-03 贵州理工学院 一种费托芳烃催化剂和制备方法及用途
CN114570412B (zh) * 2022-02-18 2024-03-08 贵州理工学院 一种费托芳烃催化剂和制备方法及用途

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GB641261A (en) 1950-08-09
FR957261A (enrdf_load_html_response) 1950-02-17

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